Conversion of low-density polyethylene into monocyclic aromatic hydrocarbons through continuous microwave pyrolysis with ex-situ dual-catalyst beds

聚烯烃 催化作用 沸石 热解 聚乙烯 低密度聚乙烯 产量(工程) 原材料 化学 有机化学 化学工程 选择性 材料科学 废物管理 核化学 复合材料 工程类 图层(电子)
作者
Yujie Peng,Xiaofei Wang,Liangliang Fan,Qi Zhang,Xian Cui,Xiaojie Tian,Qiuhao Wu,Kirk Cobb,Roger Ruan,Heng Tu,Jing Yang,Yunpu Wang
出处
期刊:Journal of Cleaner Production [Elsevier BV]
卷期号:418: 138039-138039 被引量:18
标识
DOI:10.1016/j.jclepro.2023.138039
摘要

The single-use of polyolefins-based individual protective equipment has led to the rapid generation of substantial plastic waste. This study aimed at cleaner disposal of the polyolefin waste, and carried out the continuous microwave pyrolysis (CMP) of low-density polyethylene (LDPE) over dual-catalyst beds of MCM-41 and HY. The dual-catalyzed trial was able to produce more condensate fractions with higher selectivity of monocyclic aromatic hydrocarbons (MAHs), compared with using only MCM-41 or HY zeolite. It was because the larger pore size of the MCM-41 catalyst (4.00 nm) could crack long-chain polyolefin intermediates into shorter chains. This alleviates steric and diffusional resistance while entering and exiting the micropores of the HY zeolite (0.74 × 0.74 nm). The maximum liquid yield (63.75 wt%) and MAHs selectivity (78.21%) were achieved at a catalysis temperature of 450 °C, feedstock to catalyst ratio of 8:3, and HY to MCM-41 ratio of 2:1. In addition, the performance of the CMP reactor was also compared favorably with the batch microwave pyrolysis (BMP) reactor under the same conditions. It has been found that the CMP reactor generated more MAHs products, whereas the BMP reactor was more selective for the generation of polycyclic aromatic hydrocarbons (PAHs) and gas products. The combination of CMP and the co-catalysis process offers new insight into sustainable management and value-added recovery of medical plastic waste.
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